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Master's Thesis
Author of thesis: Ing. Xin Cheng
Acad. year: 2025/2026
Supervisor: doc. Ing. Jan Boháček, Ph.D.
Reviewer: Ing. Jiří Hvožďa, Ph.D.
Droplet impact on the porous iron oxide layer is a multiphase flow problem of practical significance in spray cooling, in which the cooling spray interacts with the oxide skin formed on the surface of high-temperature metal. This paper adopts the Volume of Fluid (VOF) method realized in the open source CFD software OpenFOAM, combined with the MULES algorithm for interface capture and continuous surface force model for surface tension calculation, and conducts a numerical study of this phenomenon. All solid surfaces have a static contact angle of 20°, which is consistent with the hydrophilicity of iron oxide. The porous oxide layer is represented by a pore-resolved computational mesh instead of a volume-averaged continuum model. The grid is reconstructed from the micrograph stack of the actual oxide sample: the micrograph image is loaded into ParaView, resampled to the uniform OpenFOAM grid through the ResampleWithDataset function, denoising with a median filter, and the solid and pore regions are separated by applying an intensity threshold. The generated oxide geometry is embedded in the refined background grid through the mergeMeshes and stitchMesh functions, thus forming a single composite domain. A reference case of droplet diameter D0 = 0.1 mm and impact speed U0 = 1 m/s was established and extended it through two parameters: one is the speed parameter, U0 is 1, 2, 5 and 10 m/s respectively; the other is the droplet size parameter D0, with values of 0.1, 0.3 and 1 mm, the latter of which is obtained by rescaling the geometry using the transformPoints function. Pore penetration is quantified by two indicators extracted along the internal reference path of the oxide: the maximum penetration depth d(t) and the interface position through specific path dint (t) that changes with time. These two indicators together reveal that the early inertial dominant stage is followed by a slower capillary-driven phase. The grid of the reference case was refined to verify the sensitivity of the grid, the current non-convergence is due to several factors, which are discussed below.
Volume of Fluid (VOF), Droplet impingement, Porous iron-oxide layer, OpenFOAM
Date of defence
17.06.2026
Result of the defence
Defended (thesis was successfully defended)
Grading
D
Process of defence
The student presented the committee with the progress of the work, the results and conclusions of the thesis, and answered the supervisor's and reviewer's questions. During the defence, the student was unable to fully defend the work and did not demonstrate command of the details of the simulation; although the work employed an advanced simulation, the student was not fully familiar with its underlying details. Doc. Lízal asked about the experimental validation of the student's simulations. The student stated that no experimental work had been carried out. When asked which experimental methods could at least be used for some form of validation, the student was unable to identify any suitable method. Prof. Novotný asked whether the model was a 2D model or a genuinely axisymmetric one, and since the student had described it as axisymmetric, where the axis was located. The student indicated the position of the axis, after which the committee discussed the boundary conditions and the simulation setup. Prof. Novotný further asked which turbulence models the student had used. The student had not considered turbulence and had modelled laminar flow only. The committee discussed the suitability of this approach for the given simulation. Doc. Rudolf commented on the work and its conclusions and asked whether the velocities used were relevant to real applications. The student responded that 5 m/s was realistic. In response to a further question on whether a contact angle of 20° was realistic, the student noted that 20° could be realistic if the surface were heated. Doc. Jan asked about the physical background, namely, what happens when a liquid enters a very small, very hot pore, and how rapid the evaporation of the liquid would be. The student assumed that evaporation would be slow. Doc. Jan then asked whether the time required for the liquid to evaporate could be estimated by a simple calculation, and whether it would be on the order of milliseconds or hundreds of milliseconds. The student was unable to answer; even when guided by Doc. Jan towards thermomechanics, the student drew a T–s diagram but could not arrive at a solution. Doc. Lízal commented that the calorimetric equation might be suitable here.
Language of thesis
English
Faculty
Fakulta strojního inženýrství
Department
Heat Transfer and Fluid Flow Laboratory
Study programme
Mechanical Engineering (N-ENG-A)
Composition of Committee
doc. Ing. Pavel Charvát, Ph.D. (předseda) prof. Ing. Pavel Novotný, Ph.D. (místopředseda) doc. Ing. František Lízal, Ph.D. (člen) doc. Ing. Vít Jan, Ph.D. (člen) doc. Ing. Jiří Šremr, Ph.D. (člen) doc. Ing. Pavel Rudolf, Ph.D. (člen)
Supervisor’s reportdoc. Ing. Jan Boháček, Ph.D.
Grade proposed by supervisor: A
Reviewer’s reportIng. Jiří Hvožďa, Ph.D.
Grade proposed by reviewer: B
Responsibility: Mgr. et Mgr. Hana Odstrčilová